Process for the regeneration of an alkaline solution utilized in a process for the extraction of sulphur-containing compounds comprising a washing step
US-2018320089-A1 · Nov 8, 2018 · US
US2018291286A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018291286-A1 |
| Application number | US-201815935471-A |
| Country | US |
| Kind code | A1 |
| Filing date | Mar 26, 2018 |
| Priority date | Apr 5, 2017 |
| Publication date | Oct 11, 2018 |
| Grant date | — |
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Processes for selective extraction of surface active naphthenic acids from high total acid number crude oils for use in enhanced oil recovery are provided.
Opening claim text (preview).
1 . A method for selective extraction of surface active naphthenic acids from an acidic crude oil, comprising: providing a crude oil having a total acid number (TAN) greater than 0.4; mixing the crude oil with an aqueous solution to extract a portion of naphthenic acids from the crude oil into the aqueous solution thereby creating a crude oil/water emulsion; wherein the aqueous solution comprises water and a weak base; separating the aqueous solution containing the portion of naphthenic acids from the crude oil; wherein the aqueous solution will contain an additional portion of the crude oil; adding a salt to the aqueous solution, thereby causing the additional portion of the crude oil to separate from the aqueous solution; removing the additional portion of the crude oil from the aqueous solution; and extracting the naphthenic acids from the aqueous solution. 2 . The method of claim 1 , wherein the pH of the aqueous solution is from 10.5 to 11.5. 3 . The method of claim 2 , wherein the pH of the aqueous solution is from 10.9 to 11.2. 4 . The method of claim 1 , wherein the adding the salt to the aqueous solution occurs prior to separating the aqueous solution containing the portion of naphthenic acids from the crude oil. 5 . The method of claim 1 , wherein the water is saltwater, wherein the adding a salt act is performed by virtue of the water being saltwater. 6 . The method of claim 1 , wherein the weak base is sodium carbonate. 7 . The method of claim 1 , wherein the extracting is performed via liquid-liquid extraction. 8 . The method of claim 1 , wherein the extracting is performed via solid-phase extraction. 9 . The method of claim 1 , wherein the salt is sodium chloride. 10 . The method of claim 1 , wherein the portion of naphthenic acids extracted from the crude oil are those naphthenic acids which are soluble in solutions with a pH less than 11.1. 11 . The method of claim 1 , wherein the portion of naphthenic acids extracted from the crude oil are those naphthenic acids having a molecular weight from 200 to 700. 12 . The method of claim 1 , wherein the mixing of the crude oil with an aqueous alkaline solution is carried out in a co-current or countercurrent flow or a mixing vessel. 13 . The method of claim 1 , wherein the extraction of the portion of naphthenic acids from the aqueous solution is carried out through a multistage liquid-liquid extraction using an organic solvent. 14 . The method of claim 13 , wherein the organic solvent is a dichloromethane solvent. 15 . A method for enhanced oil recovery, comprising: selectively extracting surface active naphthenic acids from an acidic crude oil by the method of claim 1 ; injecting an aqueous alkaline solution at a pH of less than 11.1 containing the portion of naphthenic acids into a subterranean oil reservoir; recovering oil displaced by the aqueous solution. 16 . The method of claim 15 , wherein the aqueous solution containing the portion of naphthenic acids injected into the subterranean oil reservoir is saline, and is derived from seawater or produced water. 17 . The method of claim 15 , wherein the interfacial tension between aqueous solution containing the portion of naphthenic acids and the oil in the subterranean oil reservoir is reduced to less than 1 mN/m. 18 . The method of claim 15 , wherein the interfacial tension between aqueous solution containing the portion of naphthenic acids and the oil in the subterranean oil reservoir is reduced to less than 0.5 mN/m. 19 . The method of claim 15 , wherein the subterranean oil reservoir holds a crude with a total acid number less than 0.4. 20 . A method for enhanced oil recovery, comprising: selectively extracting surface active naphthenic acids from an acidic crude oil by providing a crude oil having a total acid number (TAN) greater than 0.4; contacting the crude oil with a weak anion exchange (WAX) column to recover a portion of naphthenic acids from the crude; and washing the WAX column with a solution comprising a polar solvent and an acid to recover the portion of naphthenic acids; injecting an aqueous alkaline solution at a pH of less than 11.1 containing the portion of naphthenic acids into a subterranean oil reservoir; recovering oil displaced by the aqueous solution. 21 . The method of claim 20 , wherein the aqueous solution containing the portion of naphthenic acids injected into the subterranean oil reservoir is saline, and is derived from seawater or produced water 22 . The method of claim 20 , wherein the interfacial tension between aqueous solution containing the portion of naphthenic acids and the oil in the subterranean oil reservoir is reduced to less than 1 mN/m. 23 . The method of claim 20 , wherein the interfacial tension between aqueous solution containing the portion of naphthenic acids and the oil in the subterranean oil reservoir is reduced to less than 0.5 mN/m. 24 . The method of claim 20 , wherein the subterranean oil reservoir holds a crude with a total acid number less than 0.4. 25 . The method of claim 20 , wherein the polar solvent is a high polarity solvent, such as methanol. 26 . The method of claim 20 , wherein the polar solvent is a low polarity solvent, such as dichloromethane. 27 . The method of claim 20 , wherein the washing the WAX column is performed via a series of washes starting with a solution comprising a high polarity solvent and performing successive washes with solutions comprising decreasing polarity solvents.
Naphthenic acids, TAN · CPC title
including at least one alkaline treatment step · CPC title
characterised by the use of specific surfactants · CPC title
Displacing by water · CPC title
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